CA2780543C - Prepreg - Google Patents
Prepreg Download PDFInfo
- Publication number
- CA2780543C CA2780543C CA2780543A CA2780543A CA2780543C CA 2780543 C CA2780543 C CA 2780543C CA 2780543 A CA2780543 A CA 2780543A CA 2780543 A CA2780543 A CA 2780543A CA 2780543 C CA2780543 C CA 2780543C
- Authority
- CA
- Canada
- Prior art keywords
- weight
- prepreg
- alkylacrylate
- styrene
- impregnating resin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 229920005989 resin Polymers 0.000 claims abstract description 59
- 239000011347 resin Substances 0.000 claims abstract description 59
- 229920003169 water-soluble polymer Polymers 0.000 claims abstract description 16
- 229920002818 (Hydroxyethyl)methacrylate Polymers 0.000 claims abstract description 14
- 239000000123 paper Substances 0.000 claims description 70
- 229920002472 Starch Polymers 0.000 claims description 32
- 229920001577 copolymer Polymers 0.000 claims description 32
- 235000019698 starch Nutrition 0.000 claims description 32
- 239000008107 starch Substances 0.000 claims description 30
- 229920001353 Dextrin Polymers 0.000 claims description 20
- 239000004375 Dextrin Substances 0.000 claims description 20
- 235000019425 dextrin Nutrition 0.000 claims description 20
- 239000000203 mixture Substances 0.000 claims description 20
- 239000007787 solid Substances 0.000 claims description 15
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 13
- WOBHKFSMXKNTIM-UHFFFAOYSA-N Hydroxyethyl methacrylate Chemical compound CC(=C)C(=O)OCCO WOBHKFSMXKNTIM-UHFFFAOYSA-N 0.000 claims description 12
- 239000000049 pigment Substances 0.000 claims description 11
- 229920000881 Modified starch Polymers 0.000 claims description 10
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 10
- 239000000945 filler Substances 0.000 claims description 10
- 235000019426 modified starch Nutrition 0.000 claims description 10
- 210000000988 bone and bone Anatomy 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 9
- 230000008569 process Effects 0.000 claims description 9
- 239000011248 coating agent Substances 0.000 claims description 8
- 238000000576 coating method Methods 0.000 claims description 8
- 239000011230 binding agent Substances 0.000 claims description 7
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 claims description 7
- 230000009477 glass transition Effects 0.000 claims description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 6
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 claims description 6
- 125000005250 alkyl acrylate group Chemical group 0.000 claims description 6
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 239000004408 titanium dioxide Substances 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 4
- 239000005995 Aluminium silicate Substances 0.000 claims description 3
- 235000012211 aluminium silicate Nutrition 0.000 claims description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 3
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 3
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 claims 10
- PNXMTCDJUBJHQJ-UHFFFAOYSA-N propyl prop-2-enoate Chemical compound CCCOC(=O)C=C PNXMTCDJUBJHQJ-UHFFFAOYSA-N 0.000 claims 5
- 239000000440 bentonite Substances 0.000 claims 2
- 229910000278 bentonite Inorganic materials 0.000 claims 2
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 claims 2
- 238000005470 impregnation Methods 0.000 abstract description 24
- 125000000217 alkyl group Chemical group 0.000 abstract description 4
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 abstract description 3
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 abstract description 3
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 abstract description 2
- 238000012545 processing Methods 0.000 abstract description 2
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 27
- 239000004816 latex Substances 0.000 description 26
- 229920000126 latex Polymers 0.000 description 26
- 229920001131 Pulp (paper) Polymers 0.000 description 15
- 239000011093 chipboard Substances 0.000 description 15
- 238000012360 testing method Methods 0.000 description 12
- 239000011888 foil Substances 0.000 description 11
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 101710137710 Thioesterase 1/protease 1/lysophospholipase L1 Proteins 0.000 description 9
- 229920000642 polymer Polymers 0.000 description 9
- 229920002451 polyvinyl alcohol Polymers 0.000 description 9
- 239000004372 Polyvinyl alcohol Substances 0.000 description 8
- 238000007639 printing Methods 0.000 description 7
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 6
- 238000004026 adhesive bonding Methods 0.000 description 5
- 238000009826 distribution Methods 0.000 description 5
- 239000003292 glue Substances 0.000 description 5
- 238000010030 laminating Methods 0.000 description 5
- 239000002023 wood Substances 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- 230000006835 compression Effects 0.000 description 4
- 238000003475 lamination Methods 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 239000004368 Modified starch Substances 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 3
- 230000001070 adhesive effect Effects 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 239000004815 dispersion polymer Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000005227 gel permeation chromatography Methods 0.000 description 3
- 238000000227 grinding Methods 0.000 description 3
- 239000011121 hardwood Substances 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 3
- 235000011121 sodium hydroxide Nutrition 0.000 description 3
- 239000000454 talc Substances 0.000 description 3
- 235000012222 talc Nutrition 0.000 description 3
- 229910052623 talc Inorganic materials 0.000 description 3
- 239000002966 varnish Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 2
- 241000294754 Macroptilium atropurpureum Species 0.000 description 2
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 2
- 230000009102 absorption Effects 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 239000002390 adhesive tape Substances 0.000 description 2
- 239000004411 aluminium Substances 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 239000001164 aluminium sulphate Substances 0.000 description 2
- 235000011128 aluminium sulphate Nutrition 0.000 description 2
- 239000002518 antifoaming agent Substances 0.000 description 2
- 239000004202 carbamide Substances 0.000 description 2
- BUACSMWVFUNQET-UHFFFAOYSA-H dialuminum;trisulfate;hydrate Chemical compound O.[Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O BUACSMWVFUNQET-UHFFFAOYSA-H 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000003623 enhancer Substances 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 229960004279 formaldehyde Drugs 0.000 description 2
- 235000019256 formaldehyde Nutrition 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- LEQAOMBKQFMDFZ-UHFFFAOYSA-N glyoxal Chemical compound O=CC=O LEQAOMBKQFMDFZ-UHFFFAOYSA-N 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 2
- 239000005011 phenolic resin Substances 0.000 description 2
- 229920001568 phenolic resin Polymers 0.000 description 2
- 229920002689 polyvinyl acetate Polymers 0.000 description 2
- 239000011118 polyvinyl acetate Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000004513 sizing Methods 0.000 description 2
- 239000011122 softwood Substances 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 238000004383 yellowing Methods 0.000 description 2
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 1
- FEIQOMCWGDNMHM-UHFFFAOYSA-N 5-phenylpenta-2,4-dienoic acid Chemical compound OC(=O)C=CC=CC1=CC=CC=C1 FEIQOMCWGDNMHM-UHFFFAOYSA-N 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 244000166124 Eucalyptus globulus Species 0.000 description 1
- 239000004366 Glucose oxidase Substances 0.000 description 1
- -1 Ludwig-shafen Substances 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- 239000004373 Pullulan Substances 0.000 description 1
- 229920001218 Pullulan Polymers 0.000 description 1
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Natural products C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 229920001807 Urea-formaldehyde Polymers 0.000 description 1
- 239000005083 Zinc sulfide Substances 0.000 description 1
- 125000005396 acrylic acid ester group Chemical group 0.000 description 1
- 239000002671 adjuvant Substances 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000004067 bulking agent Substances 0.000 description 1
- TUZBYYLVVXPEMA-UHFFFAOYSA-N butyl prop-2-enoate;styrene Chemical compound C=CC1=CC=CC=C1.CCCCOC(=O)C=C TUZBYYLVVXPEMA-UHFFFAOYSA-N 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- PLRSNUWXOYYMKP-UHFFFAOYSA-M chloromethyl-(3-hydroxypropyl)-dimethylazanium;chloride Chemical compound [Cl-].ClC[N+](C)(C)CCCO PLRSNUWXOYYMKP-UHFFFAOYSA-M 0.000 description 1
- 239000010431 corundum Substances 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003480 eluent Substances 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 229940015043 glyoxal Drugs 0.000 description 1
- 238000007646 gravure printing Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000011346 highly viscous material Substances 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000011120 plywood Substances 0.000 description 1
- 229920000136 polysorbate Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 235000019423 pullulan Nutrition 0.000 description 1
- 125000001453 quaternary ammonium group Chemical group 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000010561 standard procedure Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 150000003512 tertiary amines Chemical class 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 238000012876 topography Methods 0.000 description 1
- PUVAFTRIIUSGLK-UHFFFAOYSA-M trimethyl(oxiran-2-ylmethyl)azanium;chloride Chemical compound [Cl-].C[N+](C)(C)CC1CO1 PUVAFTRIIUSGLK-UHFFFAOYSA-M 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
- DRDVZXDWVBGGMH-UHFFFAOYSA-N zinc;sulfide Chemical compound [S-2].[Zn+2] DRDVZXDWVBGGMH-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/37—Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B44—DECORATIVE ARTS
- B44C—PRODUCING DECORATIVE EFFECTS; MOSAICS; TARSIA WORK; PAPERHANGING
- B44C5/00—Processes for producing special ornamental bodies
- B44C5/04—Ornamental plaques, e.g. decorative panels, decorative veneers
- B44C5/0469—Ornamental plaques, e.g. decorative panels, decorative veneers comprising a decorative sheet and a core formed by one or more resin impregnated sheets of paper
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L25/00—Compositions of, homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Compositions of derivatives of such polymers
- C08L25/02—Homopolymers or copolymers of hydrocarbons
- C08L25/04—Homopolymers or copolymers of styrene
- C08L25/08—Copolymers of styrene
- C08L25/14—Copolymers of styrene with unsaturated esters
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/18—Paper- or board-based structures for surface covering
- D21H27/22—Structures being applied on the surface by special manufacturing processes, e.g. in presses
- D21H27/26—Structures being applied on the surface by special manufacturing processes, e.g. in presses characterised by the overlay sheet or the top layers of the structures
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/24—Impregnating materials with prepolymers which can be polymerised in situ, e.g. manufacture of prepregs
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L33/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
- C08L33/04—Homopolymers or copolymers of esters
- C08L33/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, which oxygen atoms are present only as part of the carboxyl radical
- C08L33/062—Copolymers with monomers not covered by C08L33/06
- C08L33/066—Copolymers with monomers not covered by C08L33/06 containing -OH groups
Abstract
A prepreg for further processing to form a decorative paper is obtainable by impregnation of a decorative base paper with an impregnating resin solution that contains at least one styrene-alkylacrylate-hydroxyethylmethacrylate copolymer and at least one water-soluble polymer, wherein alkyl stands for methyl, ethyl, propyl, or butyl and the prepreg is notable for improved resistance to splitting as well as better adhesion and flatness.
Description
PREPREG
TECHNICAL FIELD OF THE INVENTION
The invention relates to pre-impregnates and decorative impregnates or decorative coating materials obtainable therefrom.
BACKGROUND OF THE INVENTION
Decorative coating materials, also referred to as deco-rative papers or decorative foils are primarily used as a surface coating in furniture manufacturing and interior fit-tings, particularly laminate floors. Decorative pa-per/decorative foil is understood to be printed or unprinted papers that have either been impregnated with synthetic resin or impregnated with synthetic resin and undergone sur-face treatment. Decorative papers/decorative foils are glue-bonded or adhesive-bonded to a backing panel.
Depending on the type of impregnation operation, a dis-tinction is made between decorative papers/decorative foils with a thoroughly impregnated paper core, and "prepregs", in which the paper is only partially impregnated online or off-line in the paper machine. None of the previously known pre-pregs, which contain formaldehyde-containing duroplastic resins or acrylate-containing binders that are low in for-maldehyde, satisfies all of the requirements placed on it, such as good plybond strength and good adhesion after it has been painted and stuck to a wood-based sheet material board.
In order to bond the decorative foils to wood materials such as chipboard or MDF board, the adhesives normally used are urea-based glues or polyvinyl acetate (PVAC) glues.
These do not always guarantee that the decorative foils will be bonded properly.
High pressure laminates are laminates that are produced by compressing a number of impregnated, stacked papers against each other. The structure of these laminates gener-ally includes an uppermost, transparent covering sheet (the overlay), which provides high surface resistance, a resin-impregnated decorative paper, and one or more kraft paper sheets impregnated with phenolic resin. The base (substra-tum) may be formed by hardboard and chipboard panels or ply-wood for example.
In the laminates produced according to the short cycle process (low pressure laminates), the decorative paper soaked in resin is pressed directly against a base, for ex-ample a chipboard, with the application of low pressure.
In the processing industry, very high demands are placed on the bondability and adhesion of the glued decora-tive foil. For example, adhesion must be good immediately after the gluing process, in order to prevent the freshly laminated panel from being damaged by further handling. The panels are often machined further just a few minutes to hours after the decorative foil is glued on, in sawing, milling and drilling processes, and the applied decorative foil must not separate or tear at the machined edges. The finished surfaces are often packaged for further transport as well, and adhesive tapes are used for this, being affixed directly to the decorative surface. These adhesive tapes must have sufficient adhesive strength, but they must be re-movable without residue and without damaging the decorative
TECHNICAL FIELD OF THE INVENTION
The invention relates to pre-impregnates and decorative impregnates or decorative coating materials obtainable therefrom.
BACKGROUND OF THE INVENTION
Decorative coating materials, also referred to as deco-rative papers or decorative foils are primarily used as a surface coating in furniture manufacturing and interior fit-tings, particularly laminate floors. Decorative pa-per/decorative foil is understood to be printed or unprinted papers that have either been impregnated with synthetic resin or impregnated with synthetic resin and undergone sur-face treatment. Decorative papers/decorative foils are glue-bonded or adhesive-bonded to a backing panel.
Depending on the type of impregnation operation, a dis-tinction is made between decorative papers/decorative foils with a thoroughly impregnated paper core, and "prepregs", in which the paper is only partially impregnated online or off-line in the paper machine. None of the previously known pre-pregs, which contain formaldehyde-containing duroplastic resins or acrylate-containing binders that are low in for-maldehyde, satisfies all of the requirements placed on it, such as good plybond strength and good adhesion after it has been painted and stuck to a wood-based sheet material board.
In order to bond the decorative foils to wood materials such as chipboard or MDF board, the adhesives normally used are urea-based glues or polyvinyl acetate (PVAC) glues.
These do not always guarantee that the decorative foils will be bonded properly.
High pressure laminates are laminates that are produced by compressing a number of impregnated, stacked papers against each other. The structure of these laminates gener-ally includes an uppermost, transparent covering sheet (the overlay), which provides high surface resistance, a resin-impregnated decorative paper, and one or more kraft paper sheets impregnated with phenolic resin. The base (substra-tum) may be formed by hardboard and chipboard panels or ply-wood for example.
In the laminates produced according to the short cycle process (low pressure laminates), the decorative paper soaked in resin is pressed directly against a base, for ex-ample a chipboard, with the application of low pressure.
In the processing industry, very high demands are placed on the bondability and adhesion of the glued decora-tive foil. For example, adhesion must be good immediately after the gluing process, in order to prevent the freshly laminated panel from being damaged by further handling. The panels are often machined further just a few minutes to hours after the decorative foil is glued on, in sawing, milling and drilling processes, and the applied decorative foil must not separate or tear at the machined edges. The finished surfaces are often packaged for further transport as well, and adhesive tapes are used for this, being affixed directly to the decorative surface. These adhesive tapes must have sufficient adhesive strength, but they must be re-movable without residue and without damaging the decorative
2 foil to which they stick after transporting operations are complete. The decorative foil must therefore have high ply-bond strength perpendicularly to the decorative surface af-ter it has been glued as well.
The decorative paper used in the coating materials de-scribed in the preceding is used in the white or coloured state and with or without additional printing.
With regard to their technical application properties the decorative base papers that are used as the starting ma-terials must satisfy certain requirements. These include high opacity for better coverage of the base, uniform forma-tion and grammage of the sheet for homogeneous resin absorp-tion, a high degree of resistance to light, high purity and colour evenness for good reproducibility of the pattern to be printed, wet strength to ease the impregnation process, corresponding absorbency to achieve the required degree of resin saturation, dry strength, which is important in wind-ing operations in the paper machine and during printing in the printing machine.
In order to achieve a decorative surface, the decora-tive base papers may be printed. Printing is mostly done by the rotogravure printing process, in which the printed image is transferred to the paper by means of several gravure rollers. The individual printed dots are to be transferred completely and as intensively as possible to the surface of the paper. But it is precisely in the decorative gravure printing that sometimes only a fraction of the raster points present on the gravure rollers is transferred to surface of the paper. "Missing dots", this is to say voids, occur. The printing colour often penetrates too deep into the paper
The decorative paper used in the coating materials de-scribed in the preceding is used in the white or coloured state and with or without additional printing.
With regard to their technical application properties the decorative base papers that are used as the starting ma-terials must satisfy certain requirements. These include high opacity for better coverage of the base, uniform forma-tion and grammage of the sheet for homogeneous resin absorp-tion, a high degree of resistance to light, high purity and colour evenness for good reproducibility of the pattern to be printed, wet strength to ease the impregnation process, corresponding absorbency to achieve the required degree of resin saturation, dry strength, which is important in wind-ing operations in the paper machine and during printing in the printing machine.
In order to achieve a decorative surface, the decora-tive base papers may be printed. Printing is mostly done by the rotogravure printing process, in which the printed image is transferred to the paper by means of several gravure rollers. The individual printed dots are to be transferred completely and as intensively as possible to the surface of the paper. But it is precisely in the decorative gravure printing that sometimes only a fraction of the raster points present on the gravure rollers is transferred to surface of the paper. "Missing dots", this is to say voids, occur. The printing colour often penetrates too deep into the paper
3 structure, which in turn reduces the colour intensity. The prerequisites for a good printed image with few voids and high colour intensity are thus a paper surface topography that is as smooth as possible and balanced colour acceptance behaviour of the paper surface.
For this reason, base papers are usually smoothed with soft calenders, and in some cases also with Janus calenders.
This treatment can cause the paper surface to become bruised and consequently compacted, which impairs its resin absorp-tion capability.
The properties described in the preceding are influ-enced significantly by the impregnation of the decorative base paper, that is to say by the nature of the impregnation medium used.
The impregnation resin solutions normally used for im-pregnating the decorative base papers are resins based on urea, melamine, or phenolic resins and containing formalde-hyde, and result in brittle products with poor tear propaga-tion resistance and printability.
In recent times, it has become more and more important to ensure that the impregnation resin solutions used for im-pregnating decorative base papers are free from substances that may be harmful to human health, particularly that they contain no formaldehyde. Furthermore, the components used should originate from renewable raw materials to the extent possible.
The use of a formaldehyde-free resins with a base of an acrylic acid ester styrene copolymer to produce non-
For this reason, base papers are usually smoothed with soft calenders, and in some cases also with Janus calenders.
This treatment can cause the paper surface to become bruised and consequently compacted, which impairs its resin absorp-tion capability.
The properties described in the preceding are influ-enced significantly by the impregnation of the decorative base paper, that is to say by the nature of the impregnation medium used.
The impregnation resin solutions normally used for im-pregnating the decorative base papers are resins based on urea, melamine, or phenolic resins and containing formalde-hyde, and result in brittle products with poor tear propaga-tion resistance and printability.
In recent times, it has become more and more important to ensure that the impregnation resin solutions used for im-pregnating decorative base papers are free from substances that may be harmful to human health, particularly that they contain no formaldehyde. Furthermore, the components used should originate from renewable raw materials to the extent possible.
The use of a formaldehyde-free resins with a base of an acrylic acid ester styrene copolymer to produce non-
4 yellowing prepregs is described in DE 197 28 250 Al. The disadvantage of this material is that it produces a product with poor resistance to splitting and inadequate adhesion strength after bonding.
Formaldehyde-free impregnation resin solutions for im-pregnating decorative base papers are also described in EP
09 648 248 A1 and EP 0 739 435 Al. These preferably consist of a styrene acrylic acid copolymer and polyvinyl alcohol.
Unfortunately, the paper that is impregnated with such an impregnation resin solution is also in need of further im-provement in terms of its plybond strength and adhesion af-ter bonding.
In WO 2001/11139 Al, a formaldehyde-free compound con-sisting of a binding agent, an aqueous polymer dispersion and glyoxal is suggested, with which decorative papers that are highly resistant to splitting can be produced. However, the paper impregnated with this compound does not bond well.
In WO 2009/000769 Al, a formaldehyde-free compound con-sisting of a styrene-acrylic acid ester copolymer and a starch having a particular molecular weight distribution is described. However, the properties of this prepreg with re-gard to bonding after adhesion still need improvement.
SUMMARY OF THE INVENTION
The object of the invention is therefore to provide a formaldehyde-free prepreg that does not exhibit the disad-vantages described in the preceding, and which is notable in particular for good adhesion after glueing to a wood based sheet material, high resistance to splitting even immedi-ately after glueing in the wet state, good printability, and good flatness during printing and laminating.
This object is solved with a prepreg that is obtainable by impregnating a base paper with an impregnation resin so-lution that contains at least one styrene-alkyl acrylate hy-droxyethyl(meth)acrylate copolymer and at least one water-soluble polymer, wherein alkyl may stand for methyl, ethyl, propyl and/or butyl.
A further object of the invention is a decorative paper or decorative coating material that has been produced from the aforementioned prepreg.
Surprisingly, it was found that the impregnation resin solution used according to the invention is particularly suitable, because it not only improves the resistance to splitting and bonding after adhesion to a wood based sheet material of the papers impregnated therewith, it also en-ables comparably good or even better results than those of the related art with regard to other properties such as printability, varnish penetration or yellowing.
Moreover, the problems that normally arise when hydro-philic binding agents are used for laminating (glue-bonding or adhesive bonding with the base) the impregnated papers do not occur. This means that the impregnation resin solution according to the invention may be used to produce prepregs that lend themselves well to lamination.
A further advantage consists in that the prepreg may be produced inexpensively and at high machine speeds.
DESCRIPTION OF PREFERRED EMBODIMENTS
According to the invention, prepreg is understood to mean papers that are impregnated with resin. The proportion of impregnation resin in the prepreg may preferably be 10 to 35% by weight, but particularly 12 to 30% by weight relative to the grammage of the decorative base paper.
The decorative base papers to be impregnated are papers that have not undergone any internal or surface sizing treatments. They consist essentially of wood pulp, pigments, fillers and other additives. Usual additives may be wet strength enhancers, retention agents, and fixers. Decorative base papers differ from usual papers by the much higher con-tent of fillers and higher pigment content, and the fact that they have not been subjected to internal or surface sizing.
The styrene-alkylacrylate-hydroxyethyl(meth)acrylate copolymer used according to the invention may be introduced in the form of a latex or a dispersion into the impregnation resin liquid. It seems as if the presence of hy-droxyethyl(meth)acrylate (HEMA) in the copolymer is respon-sible for the advantageous effects associated with the in-vention compared with other styrene-alkylacrylates.
The proportional quantity of the hy-droxyethyl(meth)acrylate in the styrene-alkylacrylate-hydroxyethyl(meth)acrylate copolymer may preferably be from 0.5 to 20% by weight relative to the mass of the acrylate fraction, particularly 1 to 10% by weight. It has proven particularly advantageous if the fraction of the comonomer used according to the invention is between 3 and 8% by weight.
The alkyl in the styrene-alkylacrylate is preferably an ethyl or butyl. Copolymers may be used as mixtures of these alkyl groups in the alkylacrylate fraction.
It is particularly preferred if the copolymer used ac-cording to the invention has a glass transition temperature (TG) from 35 to 50 C.
The water-soluble polymer used according to the inven-tion in the impregnation resin is preferably starch or a starch dextrin.
A preferred starch dextrin or modified starch may have a molecular weight distribution, expressed by a polydisper-sity index Mw/Mn, of at least 6. Starches that have a polydispersity index from 6 to 20 are preferred. In one par-ticular variant, a modified starch preferably has the fol-lowing molecular weight distribution of starch molecules:
- not more than 6% by weight of molecules having a mo-lecular weight from 0 to 1,000 g/mol,
Formaldehyde-free impregnation resin solutions for im-pregnating decorative base papers are also described in EP
09 648 248 A1 and EP 0 739 435 Al. These preferably consist of a styrene acrylic acid copolymer and polyvinyl alcohol.
Unfortunately, the paper that is impregnated with such an impregnation resin solution is also in need of further im-provement in terms of its plybond strength and adhesion af-ter bonding.
In WO 2001/11139 Al, a formaldehyde-free compound con-sisting of a binding agent, an aqueous polymer dispersion and glyoxal is suggested, with which decorative papers that are highly resistant to splitting can be produced. However, the paper impregnated with this compound does not bond well.
In WO 2009/000769 Al, a formaldehyde-free compound con-sisting of a styrene-acrylic acid ester copolymer and a starch having a particular molecular weight distribution is described. However, the properties of this prepreg with re-gard to bonding after adhesion still need improvement.
SUMMARY OF THE INVENTION
The object of the invention is therefore to provide a formaldehyde-free prepreg that does not exhibit the disad-vantages described in the preceding, and which is notable in particular for good adhesion after glueing to a wood based sheet material, high resistance to splitting even immedi-ately after glueing in the wet state, good printability, and good flatness during printing and laminating.
This object is solved with a prepreg that is obtainable by impregnating a base paper with an impregnation resin so-lution that contains at least one styrene-alkyl acrylate hy-droxyethyl(meth)acrylate copolymer and at least one water-soluble polymer, wherein alkyl may stand for methyl, ethyl, propyl and/or butyl.
A further object of the invention is a decorative paper or decorative coating material that has been produced from the aforementioned prepreg.
Surprisingly, it was found that the impregnation resin solution used according to the invention is particularly suitable, because it not only improves the resistance to splitting and bonding after adhesion to a wood based sheet material of the papers impregnated therewith, it also en-ables comparably good or even better results than those of the related art with regard to other properties such as printability, varnish penetration or yellowing.
Moreover, the problems that normally arise when hydro-philic binding agents are used for laminating (glue-bonding or adhesive bonding with the base) the impregnated papers do not occur. This means that the impregnation resin solution according to the invention may be used to produce prepregs that lend themselves well to lamination.
A further advantage consists in that the prepreg may be produced inexpensively and at high machine speeds.
DESCRIPTION OF PREFERRED EMBODIMENTS
According to the invention, prepreg is understood to mean papers that are impregnated with resin. The proportion of impregnation resin in the prepreg may preferably be 10 to 35% by weight, but particularly 12 to 30% by weight relative to the grammage of the decorative base paper.
The decorative base papers to be impregnated are papers that have not undergone any internal or surface sizing treatments. They consist essentially of wood pulp, pigments, fillers and other additives. Usual additives may be wet strength enhancers, retention agents, and fixers. Decorative base papers differ from usual papers by the much higher con-tent of fillers and higher pigment content, and the fact that they have not been subjected to internal or surface sizing.
The styrene-alkylacrylate-hydroxyethyl(meth)acrylate copolymer used according to the invention may be introduced in the form of a latex or a dispersion into the impregnation resin liquid. It seems as if the presence of hy-droxyethyl(meth)acrylate (HEMA) in the copolymer is respon-sible for the advantageous effects associated with the in-vention compared with other styrene-alkylacrylates.
The proportional quantity of the hy-droxyethyl(meth)acrylate in the styrene-alkylacrylate-hydroxyethyl(meth)acrylate copolymer may preferably be from 0.5 to 20% by weight relative to the mass of the acrylate fraction, particularly 1 to 10% by weight. It has proven particularly advantageous if the fraction of the comonomer used according to the invention is between 3 and 8% by weight.
The alkyl in the styrene-alkylacrylate is preferably an ethyl or butyl. Copolymers may be used as mixtures of these alkyl groups in the alkylacrylate fraction.
It is particularly preferred if the copolymer used ac-cording to the invention has a glass transition temperature (TG) from 35 to 50 C.
The water-soluble polymer used according to the inven-tion in the impregnation resin is preferably starch or a starch dextrin.
A preferred starch dextrin or modified starch may have a molecular weight distribution, expressed by a polydisper-sity index Mw/Mn, of at least 6. Starches that have a polydispersity index from 6 to 20 are preferred. In one par-ticular variant, a modified starch preferably has the fol-lowing molecular weight distribution of starch molecules:
- not more than 6% by weight of molecules having a mo-lecular weight from 0 to 1,000 g/mol,
- 5 to 20% by weight of molecules having a molecular weight between 1,000 and 5,000 g/mol, - 20 to 40% by weight of molecules having a molecular weight between 5,000 and 25,000 g/mol, - 20 to 45% by weight of molecules having a molecular weight between 25,000 and 200,000 g/mol, to 22% by weight of molecules having a molecular weight between 200,000 and 1,000,000 g/mol, 0.5 to 5% by weight of molecules having a molecular weight greater than 1,000,000 g/mol.
Such a modified starch is available commercially. The polydispersity index is usually expressed as the ratio be-tween the weight-average and the number-average molar mass Mw/Mn. It provides information about the width of the mo-lecular weight distribution curve.
The molecular weight distribution of modified starches was determined in the normal way by the starch manufacturer using gel permeation chromatography (GPC). The GPC analysis was performed using a chromatograph with Shodex KS columns.
The eluent was 0.05 M NaOH at a flowthrough rate of 1 ml/min. Calibration was carried out using pullulan standards having known molecular weights.
The proportion of water-soluble polymer/polymer latex in the impregnation resin solution is preferably from 80/20 to 20/80, wherein a proportion of 45/55 to 65/35 and par-ticularly 50/50 to 60/40 relative to the mass of the impreg-nation resin (atro) is preferred. The water-soluble polymer is preferably selected from starches or starch derivatives, particularly starch dextrin, which can be produced from re-newable raw materials. According to another variation of the invention, polyvinyl alcohol may be used additionally.
The impregnated resin solution may contain pigments and/or fillers. The quantity of the pigment and/or filler may be from 1 to 30% by weight, particularly 2 to 20% by weight. Quantities are given relative to the mass of the binder (bone dry). For the present purposes, the term binder is used to describe the mixture containing the polymer latex and the water-soluble polymer.
The impregnation resin solution used to manufacture the prepregs according to the invention has a total solid con-tent relative to dry weight from 9 to 40% by weight, pref-erably 20 to 35% by weight, and particularly preferably 26 to 30% by weight.
In order to produce the impregnation resin solution, first the starch may be prepared, either cold, that is to say it is dissolved in water at room temperature up to a temperature not exceeding 60 C, or it is boiled at about 120 to 145 C. This produces a 40 to 45% suspension with a pH value of about 5 to 6. In the next step, an approximately 50% latex dispersion with a pH value from 5 to 10 is added, taking into account the desired solid content and starch/latex ratio. In a further step, pigment or filler may be added.
The base paper to be impregnated according to the in-vention may contain a large fraction of a pigment or filler.
The percentage of filler in the base paper may be up to 55%
by weight, particularly 8 to 45% by weight relative to the grammage (basis weight). Suitable pigments and fillers are for example titanium dioxide, talcum, zinc sulphide, kaolin, aluminium oxide, calcium carbonate, corundum, silicates of aluminium and magnesium, or mixtures thereof.
The wood pulp content used for producing the base pa-pers may be softwood pulps (long fibre pulps) and/or hard-wood pulps (short fibre pulps). Cotton fibres and mixtures thereof with the aforementioned wood pulp types may also be used. For example, a mixture of softwood and hardwood pulps in ratios from 10:90 to 90:10, particularly from 20:80 to 80:20 is particularly preferred. However, the use of 100% by weight hardwood pulp has also proven advantageous. Percent-ages refer to the mass of the pulps (bone dry).
The pulp mixture may preferably contain cationically modified pulp fibres in a quantity of at least 5% by weight relative to the weight of the pulp mixture. A proportion from 10 to 50% by weight, particularly 10 to 20% by weight of the cationically modified wood pulp in the wood pulp mix-ture has proven particularly advantageous. The cationic modification of the pulp fibres may be carried out by react-ing the fibres with an epichlorhydrin resin and a tertiary amine, or in a reaction with quaternary ammonium chlorides such as chlorohydroxypropyl trimethylammonium chloride or glycidyl trimethyl ammonium chloride. Cationically modified wood pulps and the production thereof are known for example from the publication DAS PAPIER, vol. 12 (1980), pp. 575-579.
The base papers may be produced on a Fourdrinier paper machine or a Yankee paper machine. For this, the wood pulp mixture may be ground with a stock consistency of 2 to 5% by weight to a grinding degree of 10 to 45 SR. The bulking agents such as titanium dioxide and talcum, and the wet strength enhancer may be added to the wood pulp mixture and mixed thoroughly in a mixing chest. The highly viscous sub-stance obtained may be diluted to a stock consistency of about 1%, and if necessary further adjuvants such as reten-tion agents, antifoaming agents, aluminium sulphate and other auxiliary substances listed previously may be added.
This thin stock is passed to the wire section via the head-box of the paper machine. A non-woven sheet of fibres is formed, and after dewatering the base paper is obtained and subsequently dried. The grammages of the papers produced may be from 15 to 300 g/m2. However, base papers with a weight per unit area of 40 to 100 g/m2 are preferred.
The impregnation resin solution to be used according to the invention may be applied in the paper machine or offline by spraying, impregnation, roller application or blade ap-plicator (doctor blade). Application using a size press or a film press is particularly preferred.
The impregnated papers are dried in the usual way using IR or roller driers in a temperature range from 120 to 180 C until a residual moisture content of 2 to 6% is reached.
After drying, the papers impregnated in this way (pre-pregs) may be printed and varnished, and then laminated onto various substrates, such as chipboard or fibreboard using standard methods.
The following examples will serve to explain the inven-tion in greater detail. Unless indicated otherwise, values given in percentage by weight refer to the weight of the wood pulp. The proportion means the ratio of masses or the weight ratio.
=
EXAMPLES
Example V-1 (comparison) A wood pulp suspension was prepared by grinding a wood pulp mixture of 80% by weight eucalyptus pulp and 20% conif-erous wood sulphate pulp with a stock consistency of 5% to a grinding degree of 33 SR (Schopper-Riegler). Then, 1.8% by weight epichlorohydrin resin was added as a wet strength en-hancer. This wood pulp suspension was adjusted to a pH value of 6.5 with aluminium sulphate. After that, a mixture of 30%
by weight titanium dioxide and 5% by weight talcum, 0.11% by weight of a retention agent and 0.03% by weight of an anti-foaming agent was added to the wood pulp suspension and a decorative base paper with a weight per unit area of about 50 g/m2 and an ash content of about 23% by weight was pro-duced. Weight information refers to the weight of the wood pulp (atro).
This base paper was impregnated on both sides with an aqueous resin solution of about 25% by weight solid content containing starch dextrin (EMDEX B1102, manufactured by Em-sland-Starke, Emlichheim) and styrene-butylacrylate copoly-mer latex (PLEXT01 X4340, manufactured by Polymer Latex, Marl) in a ratio of 55:45 in a size press. For this, first a feedstock of 45% starch dextrin was prepared and diluted with water to a concentration of 25% by weight. Them the matching quantity of the 50% aqueous polymer dispersion was added and the polymer solution obtained was diluted with wa-ter to a solid content of 30% by weight and adjusted to a pH
of 8.0 with caustic soda.
The impregnated paper was then dried at a temperature of about 120 C until its residual moisture reached a level of 2.5%. The quantity of impregnating resin solution for ap-plication after drying was 10 g/m2.
The glass transition temperature Tg of the latex (co-polymer) used, PLEXTOL X4340, is 28 C.
Example A-1 (invention) The base paper produced as described in Example V-1 was impregnated in a size press with an aqueous resin solution having a solid content of 25%, containing starch dextrin EM-DEX E1102 and a latex trial product 1, which was manufac-tured in the same way as PLEXTOL X4340, but in which 3% of the butyl acrylate was replaced with hydroxyethyl methacry-late (HEMA), in a ratio of 55:45. The styrene-butylacrylate-(hydroxyethyl methacrylate)-latex has a glass transition temperature Tg of 36 C.
Example B-1 (invention) The base paper produced as described in Example V-1 was impregnated in a size press with an aqueous resin solution having a solid content of 25%, containing starch dextrin EM-DEXO B1102 and a latex trial product 2, which was manufac-tured in the same way as PLEXTOLO X4340, but in which 6% of the butyl acrylate was replaced with hydroxyethyl methacry-late (HEMA), in a ratio of 55:45. The styrene-butylacrylate-hydroxyethyl methacrylate-polymer has a glass transition temperature Tg of 40 C.
Example B-2 (invention) The prepreg was produced in the same way as prepreg B-1, but the ratio of starch dextrin to latex trial product 2 in the impregnation resin solution was 40:60.
Example B-3 (invention) The prepreg was produced in the same way as prepreg B-1, but the ratio of starch dextrin to latex trial product 2 in the impregnation resin solution was 25:75.
Example C-1 through C-3 The prepregs were produced in the same way as Examples B-1 through B-3, but the latex used was trial product 3 ob-tained from Polymer Latex, Marl. Latex trial product 3 is based on a styrene-ethylacrylate-polymer, with 6 % of the ethylacrylate monomer replaced by hydroxyethyl methacrylate (HEMA). The styrene-ethylacrylate-(hydroxyethyl methacry-late)-latex has a glass transition temperature Tg of 39 C.
The impregantion resin solutions used had a latex to starch dextrin ration of 45 : 55 for example C-1, 60 : 40 for exam-ples C-2 and 75 : 25 for example C-3 Example V-2 (comparison) The base paper produced as described in Example V-1 was impregnated in a size press with an aqueous resin solution having a solid content of 25%, containing starch dextrin EM-DEXO B1102, polyvinyl alcohol MOWIOLe 4-98 (manufactured by Kuraray Europe GmbH, Frankfurt) and latex PLEXTOLO X4340, in a ratio of 40:15:45.
First a 45% starch dextrin formulation and a 10%
MOwIOLO formulation prepared correspondingly were mixed with the above. Then the corresponding quantity of 50% aqueous polymer dispersion was added and the polymer solution ob-tained was diluted with until the solid content was 30% by weight, and adjusted to pH 8.0 with caustic soda.
Example A-2 (invention) The base paper produced as described in Example V-1 was impregnated in a size press with an aqueous resin solution having a solid content of 25%, containing starch dextrin EM-DEXO B1102, polyvinyl alcohol MOWIOLO 4-98 and latex trial product 1, in a ratio of 40:15:45.
Example B-4 (invention) The base paper produced as described in Example V-1 was impregnated in a size press with an aqueous resin solution having a solid content of 25%, containing starch dextrin EM-DEXO B1102, polyvinyl alcohol MOWIOLO 4-98 and latex trial product 2, in a ratio of 40:15:45.
Example 3-4 (invention) The base paper produced as described in Example V-1 was impregnated in a size press with an aqueous resin solution having a solid content of 25%, containing starch dextrin EM-DEXO B1102, polyvinyl alcohol MOWIOLO 4-98 and latex trial product 2, in a ratio of 10:15:75.
Table 1 shows the results of tests of the papers treated according to the invention compared with the prior art. The following properties were tested:
Ply bond strength (parameter for resistance to splitting) The measurement was taken on the prepreg with the aid of the emco IBT Internal Bond Tester (manufactured by emco GmbH, Leipzig, Germany) in accordance with the standardised test method TAPPI 833-om 94. The material to be tested is cut into a 1-inch wide strip and attached between an anvil and 5 aluminium brackets by adhesion using double-sided ad-hesive tape, and compressed in the compression mechanism for a defined compression time and with a defined compression force. Five samples are placed in the sample holder of the impact mechanism simultaneously and subjected to an impact force with a weight of 30 kg.
Dry breaking strength and wet breaking strength Measurement was performed on the prepreg in accordance with DIN-EN-ISO-1924 T2.
The test of bond strength and the TESA test are per-formed on varnished samples of the prepreg that have been laminated onto a chipboard panel.
Varnish of the prepreg The prepreg samples are preheated for 60 seconds at 160 C. Then, 10 1 g/m2 of the acid-hardening varnish system IV-49 manufactured by Plantagchemie, Detmold, is spread over them with a doctor blade. The samples are dried by laying them horizontally in a drying kiln for 45 seconds at 160 C.
Lamination of the prepreg The varnished prepreg is attached to a chipboard panel using a laboratory laminating calender. Standard commercial chipboard panels (20 x 20 cm) are used. A urea-resin-glue solution (Kaurit Leim 122 manufactured by BASF AG, Ludwig-shafen, powder dissolved in water with 50% solid content) is applied to one side of the chipboard panel with a doctor knife, the glue application is 35 5 g/m2 relative to solid content. The varnished prepreg sheet is placed on top of the sized chipboard surface, the varnished side of the sheet facing away from the chipboard and the sheet protruding about 2 cm beyond the edges of the chipboard on all sides.
The chipboard panel with the varnished prepreg is then pushed through the laminating calender, where a contact pressure of 80N/mm is applied, the temperature of the com-pression rollers is 180 C, and the feed speed is 2 m/min.
Adhesive strength The test of adhesion begins immediately after lamina-tion. For this purpose, the approximately prepreg strip, ex-tending about 2 cm over the sides of the chipboard panel is cut perpendicularly to the edge of the panel. The width of the strips and their distance from each other are both 12 mm.
Each protruding strip is drawn sharply over a triangu-lar bar by hand at an angle of 60 to the chipboard panel.
This tugging test is carried out immediately following lami-nation, and then repeated after a further 2 minutes, 5 min-utes, 10 minutes, 30 minutes and 24 hours. The area that is no longer or no longer completely covered by the prepreg af-ter the tugging operations is evaluated. The evaluation is recorded in the form of scores (score 1 = very good to score
Such a modified starch is available commercially. The polydispersity index is usually expressed as the ratio be-tween the weight-average and the number-average molar mass Mw/Mn. It provides information about the width of the mo-lecular weight distribution curve.
The molecular weight distribution of modified starches was determined in the normal way by the starch manufacturer using gel permeation chromatography (GPC). The GPC analysis was performed using a chromatograph with Shodex KS columns.
The eluent was 0.05 M NaOH at a flowthrough rate of 1 ml/min. Calibration was carried out using pullulan standards having known molecular weights.
The proportion of water-soluble polymer/polymer latex in the impregnation resin solution is preferably from 80/20 to 20/80, wherein a proportion of 45/55 to 65/35 and par-ticularly 50/50 to 60/40 relative to the mass of the impreg-nation resin (atro) is preferred. The water-soluble polymer is preferably selected from starches or starch derivatives, particularly starch dextrin, which can be produced from re-newable raw materials. According to another variation of the invention, polyvinyl alcohol may be used additionally.
The impregnated resin solution may contain pigments and/or fillers. The quantity of the pigment and/or filler may be from 1 to 30% by weight, particularly 2 to 20% by weight. Quantities are given relative to the mass of the binder (bone dry). For the present purposes, the term binder is used to describe the mixture containing the polymer latex and the water-soluble polymer.
The impregnation resin solution used to manufacture the prepregs according to the invention has a total solid con-tent relative to dry weight from 9 to 40% by weight, pref-erably 20 to 35% by weight, and particularly preferably 26 to 30% by weight.
In order to produce the impregnation resin solution, first the starch may be prepared, either cold, that is to say it is dissolved in water at room temperature up to a temperature not exceeding 60 C, or it is boiled at about 120 to 145 C. This produces a 40 to 45% suspension with a pH value of about 5 to 6. In the next step, an approximately 50% latex dispersion with a pH value from 5 to 10 is added, taking into account the desired solid content and starch/latex ratio. In a further step, pigment or filler may be added.
The base paper to be impregnated according to the in-vention may contain a large fraction of a pigment or filler.
The percentage of filler in the base paper may be up to 55%
by weight, particularly 8 to 45% by weight relative to the grammage (basis weight). Suitable pigments and fillers are for example titanium dioxide, talcum, zinc sulphide, kaolin, aluminium oxide, calcium carbonate, corundum, silicates of aluminium and magnesium, or mixtures thereof.
The wood pulp content used for producing the base pa-pers may be softwood pulps (long fibre pulps) and/or hard-wood pulps (short fibre pulps). Cotton fibres and mixtures thereof with the aforementioned wood pulp types may also be used. For example, a mixture of softwood and hardwood pulps in ratios from 10:90 to 90:10, particularly from 20:80 to 80:20 is particularly preferred. However, the use of 100% by weight hardwood pulp has also proven advantageous. Percent-ages refer to the mass of the pulps (bone dry).
The pulp mixture may preferably contain cationically modified pulp fibres in a quantity of at least 5% by weight relative to the weight of the pulp mixture. A proportion from 10 to 50% by weight, particularly 10 to 20% by weight of the cationically modified wood pulp in the wood pulp mix-ture has proven particularly advantageous. The cationic modification of the pulp fibres may be carried out by react-ing the fibres with an epichlorhydrin resin and a tertiary amine, or in a reaction with quaternary ammonium chlorides such as chlorohydroxypropyl trimethylammonium chloride or glycidyl trimethyl ammonium chloride. Cationically modified wood pulps and the production thereof are known for example from the publication DAS PAPIER, vol. 12 (1980), pp. 575-579.
The base papers may be produced on a Fourdrinier paper machine or a Yankee paper machine. For this, the wood pulp mixture may be ground with a stock consistency of 2 to 5% by weight to a grinding degree of 10 to 45 SR. The bulking agents such as titanium dioxide and talcum, and the wet strength enhancer may be added to the wood pulp mixture and mixed thoroughly in a mixing chest. The highly viscous sub-stance obtained may be diluted to a stock consistency of about 1%, and if necessary further adjuvants such as reten-tion agents, antifoaming agents, aluminium sulphate and other auxiliary substances listed previously may be added.
This thin stock is passed to the wire section via the head-box of the paper machine. A non-woven sheet of fibres is formed, and after dewatering the base paper is obtained and subsequently dried. The grammages of the papers produced may be from 15 to 300 g/m2. However, base papers with a weight per unit area of 40 to 100 g/m2 are preferred.
The impregnation resin solution to be used according to the invention may be applied in the paper machine or offline by spraying, impregnation, roller application or blade ap-plicator (doctor blade). Application using a size press or a film press is particularly preferred.
The impregnated papers are dried in the usual way using IR or roller driers in a temperature range from 120 to 180 C until a residual moisture content of 2 to 6% is reached.
After drying, the papers impregnated in this way (pre-pregs) may be printed and varnished, and then laminated onto various substrates, such as chipboard or fibreboard using standard methods.
The following examples will serve to explain the inven-tion in greater detail. Unless indicated otherwise, values given in percentage by weight refer to the weight of the wood pulp. The proportion means the ratio of masses or the weight ratio.
=
EXAMPLES
Example V-1 (comparison) A wood pulp suspension was prepared by grinding a wood pulp mixture of 80% by weight eucalyptus pulp and 20% conif-erous wood sulphate pulp with a stock consistency of 5% to a grinding degree of 33 SR (Schopper-Riegler). Then, 1.8% by weight epichlorohydrin resin was added as a wet strength en-hancer. This wood pulp suspension was adjusted to a pH value of 6.5 with aluminium sulphate. After that, a mixture of 30%
by weight titanium dioxide and 5% by weight talcum, 0.11% by weight of a retention agent and 0.03% by weight of an anti-foaming agent was added to the wood pulp suspension and a decorative base paper with a weight per unit area of about 50 g/m2 and an ash content of about 23% by weight was pro-duced. Weight information refers to the weight of the wood pulp (atro).
This base paper was impregnated on both sides with an aqueous resin solution of about 25% by weight solid content containing starch dextrin (EMDEX B1102, manufactured by Em-sland-Starke, Emlichheim) and styrene-butylacrylate copoly-mer latex (PLEXT01 X4340, manufactured by Polymer Latex, Marl) in a ratio of 55:45 in a size press. For this, first a feedstock of 45% starch dextrin was prepared and diluted with water to a concentration of 25% by weight. Them the matching quantity of the 50% aqueous polymer dispersion was added and the polymer solution obtained was diluted with wa-ter to a solid content of 30% by weight and adjusted to a pH
of 8.0 with caustic soda.
The impregnated paper was then dried at a temperature of about 120 C until its residual moisture reached a level of 2.5%. The quantity of impregnating resin solution for ap-plication after drying was 10 g/m2.
The glass transition temperature Tg of the latex (co-polymer) used, PLEXTOL X4340, is 28 C.
Example A-1 (invention) The base paper produced as described in Example V-1 was impregnated in a size press with an aqueous resin solution having a solid content of 25%, containing starch dextrin EM-DEX E1102 and a latex trial product 1, which was manufac-tured in the same way as PLEXTOL X4340, but in which 3% of the butyl acrylate was replaced with hydroxyethyl methacry-late (HEMA), in a ratio of 55:45. The styrene-butylacrylate-(hydroxyethyl methacrylate)-latex has a glass transition temperature Tg of 36 C.
Example B-1 (invention) The base paper produced as described in Example V-1 was impregnated in a size press with an aqueous resin solution having a solid content of 25%, containing starch dextrin EM-DEXO B1102 and a latex trial product 2, which was manufac-tured in the same way as PLEXTOLO X4340, but in which 6% of the butyl acrylate was replaced with hydroxyethyl methacry-late (HEMA), in a ratio of 55:45. The styrene-butylacrylate-hydroxyethyl methacrylate-polymer has a glass transition temperature Tg of 40 C.
Example B-2 (invention) The prepreg was produced in the same way as prepreg B-1, but the ratio of starch dextrin to latex trial product 2 in the impregnation resin solution was 40:60.
Example B-3 (invention) The prepreg was produced in the same way as prepreg B-1, but the ratio of starch dextrin to latex trial product 2 in the impregnation resin solution was 25:75.
Example C-1 through C-3 The prepregs were produced in the same way as Examples B-1 through B-3, but the latex used was trial product 3 ob-tained from Polymer Latex, Marl. Latex trial product 3 is based on a styrene-ethylacrylate-polymer, with 6 % of the ethylacrylate monomer replaced by hydroxyethyl methacrylate (HEMA). The styrene-ethylacrylate-(hydroxyethyl methacry-late)-latex has a glass transition temperature Tg of 39 C.
The impregantion resin solutions used had a latex to starch dextrin ration of 45 : 55 for example C-1, 60 : 40 for exam-ples C-2 and 75 : 25 for example C-3 Example V-2 (comparison) The base paper produced as described in Example V-1 was impregnated in a size press with an aqueous resin solution having a solid content of 25%, containing starch dextrin EM-DEXO B1102, polyvinyl alcohol MOWIOLe 4-98 (manufactured by Kuraray Europe GmbH, Frankfurt) and latex PLEXTOLO X4340, in a ratio of 40:15:45.
First a 45% starch dextrin formulation and a 10%
MOwIOLO formulation prepared correspondingly were mixed with the above. Then the corresponding quantity of 50% aqueous polymer dispersion was added and the polymer solution ob-tained was diluted with until the solid content was 30% by weight, and adjusted to pH 8.0 with caustic soda.
Example A-2 (invention) The base paper produced as described in Example V-1 was impregnated in a size press with an aqueous resin solution having a solid content of 25%, containing starch dextrin EM-DEXO B1102, polyvinyl alcohol MOWIOLO 4-98 and latex trial product 1, in a ratio of 40:15:45.
Example B-4 (invention) The base paper produced as described in Example V-1 was impregnated in a size press with an aqueous resin solution having a solid content of 25%, containing starch dextrin EM-DEXO B1102, polyvinyl alcohol MOWIOLO 4-98 and latex trial product 2, in a ratio of 40:15:45.
Example 3-4 (invention) The base paper produced as described in Example V-1 was impregnated in a size press with an aqueous resin solution having a solid content of 25%, containing starch dextrin EM-DEXO B1102, polyvinyl alcohol MOWIOLO 4-98 and latex trial product 2, in a ratio of 10:15:75.
Table 1 shows the results of tests of the papers treated according to the invention compared with the prior art. The following properties were tested:
Ply bond strength (parameter for resistance to splitting) The measurement was taken on the prepreg with the aid of the emco IBT Internal Bond Tester (manufactured by emco GmbH, Leipzig, Germany) in accordance with the standardised test method TAPPI 833-om 94. The material to be tested is cut into a 1-inch wide strip and attached between an anvil and 5 aluminium brackets by adhesion using double-sided ad-hesive tape, and compressed in the compression mechanism for a defined compression time and with a defined compression force. Five samples are placed in the sample holder of the impact mechanism simultaneously and subjected to an impact force with a weight of 30 kg.
Dry breaking strength and wet breaking strength Measurement was performed on the prepreg in accordance with DIN-EN-ISO-1924 T2.
The test of bond strength and the TESA test are per-formed on varnished samples of the prepreg that have been laminated onto a chipboard panel.
Varnish of the prepreg The prepreg samples are preheated for 60 seconds at 160 C. Then, 10 1 g/m2 of the acid-hardening varnish system IV-49 manufactured by Plantagchemie, Detmold, is spread over them with a doctor blade. The samples are dried by laying them horizontally in a drying kiln for 45 seconds at 160 C.
Lamination of the prepreg The varnished prepreg is attached to a chipboard panel using a laboratory laminating calender. Standard commercial chipboard panels (20 x 20 cm) are used. A urea-resin-glue solution (Kaurit Leim 122 manufactured by BASF AG, Ludwig-shafen, powder dissolved in water with 50% solid content) is applied to one side of the chipboard panel with a doctor knife, the glue application is 35 5 g/m2 relative to solid content. The varnished prepreg sheet is placed on top of the sized chipboard surface, the varnished side of the sheet facing away from the chipboard and the sheet protruding about 2 cm beyond the edges of the chipboard on all sides.
The chipboard panel with the varnished prepreg is then pushed through the laminating calender, where a contact pressure of 80N/mm is applied, the temperature of the com-pression rollers is 180 C, and the feed speed is 2 m/min.
Adhesive strength The test of adhesion begins immediately after lamina-tion. For this purpose, the approximately prepreg strip, ex-tending about 2 cm over the sides of the chipboard panel is cut perpendicularly to the edge of the panel. The width of the strips and their distance from each other are both 12 mm.
Each protruding strip is drawn sharply over a triangu-lar bar by hand at an angle of 60 to the chipboard panel.
This tugging test is carried out immediately following lami-nation, and then repeated after a further 2 minutes, 5 min-utes, 10 minutes, 30 minutes and 24 hours. The area that is no longer or no longer completely covered by the prepreg af-ter the tugging operations is evaluated. The evaluation is recorded in the form of scores (score 1 = very good to score
6 = unsatisfactory).
TESA test The TESA test is carried out on the basis of company standard IHD-W-463 of the Institut fur Holztechnologie Dres-den. First, the laminated panels are stored fro 24 h. Then, TESA film strips (TESA film type 4104) approximately 15 cm.
wide are applied to the laminated panel in the feed direc-tion of the laminating calender and perpendicularly thereto and rendered bubble-free with a test roller (10 kg). The TESA strips are torn off sharply by hand at an angle of 30 at several different times (immediately, 1 h, 2h). The area below the torn off test strip is evaluated, ideally the pa-per does not split. The evaluation of TESA resistance is re-corded in the form of scores (score 1 = very good to score 6 = unsatisfactory).
The results of the tests shown in table 1 show that in-creasing the hydroxyethyl methacrylate content in the sty-rene-alkylacrylate polymer in the impregnation resin solu-tion from 0% by weight to 3% by weight, and further to 6% by weight, relative to the acrylate fraction in each case, also causes increases in the structural strength and the dry and wet breaking strengths of the prepreg, and at the same time improves the adhesion of the prepreg to the chipboard panel, and TESA resistance is also improved. This improvement is obtained both when starch dextrin is used as the water-soluble polymer and when mixtures of starch dextrin and polyvinyl alcohol are used as such. A further increase may be realised by raising the proportion of the styrene-alkyl acrylate-hydroxyethyl(meth)acrylate copolymer.
, _______________________________________________________________________________ __________________________________ Latex Latex Latex Latex Dextrin PVA Ply bond Dry Wet Adhesion TESA
Plex- trial trial trial EMDEX Mowiol strength breaking breaking test tol product product 2 product 3 B1102 4-98 strength strength UF glue 2h X4340 1 3% 6% HEMA 6% HEMA
HEMA
MD/CD MD/CD
Tg= Tg= 40 C Tg= 39 C
28 C Tg= 36 C
, _______________________________________________________________________________ __________________________________ %/wt %/wt %/wt %/wt %/wt J/m2 N/mm- N/mm2 Score Score (bone (bone (bone (bone (bone dry) dry) dry) dry) dry) o , N.) m B-1 45 55 0 1620 74/42 30/25 1 2 g 0.
76/41 38/29 1 1 w N.) N.) 75 / 41 31 / 27 1 2 r r io 76 / 43 39 / 30 2,5 1 0 , _______________________________________________________________________________ __________________________________ .
69/41 23/24 1 2,5 Table 1 above shows the composition of impregnating resin solution and test results.
TESA test The TESA test is carried out on the basis of company standard IHD-W-463 of the Institut fur Holztechnologie Dres-den. First, the laminated panels are stored fro 24 h. Then, TESA film strips (TESA film type 4104) approximately 15 cm.
wide are applied to the laminated panel in the feed direc-tion of the laminating calender and perpendicularly thereto and rendered bubble-free with a test roller (10 kg). The TESA strips are torn off sharply by hand at an angle of 30 at several different times (immediately, 1 h, 2h). The area below the torn off test strip is evaluated, ideally the pa-per does not split. The evaluation of TESA resistance is re-corded in the form of scores (score 1 = very good to score 6 = unsatisfactory).
The results of the tests shown in table 1 show that in-creasing the hydroxyethyl methacrylate content in the sty-rene-alkylacrylate polymer in the impregnation resin solu-tion from 0% by weight to 3% by weight, and further to 6% by weight, relative to the acrylate fraction in each case, also causes increases in the structural strength and the dry and wet breaking strengths of the prepreg, and at the same time improves the adhesion of the prepreg to the chipboard panel, and TESA resistance is also improved. This improvement is obtained both when starch dextrin is used as the water-soluble polymer and when mixtures of starch dextrin and polyvinyl alcohol are used as such. A further increase may be realised by raising the proportion of the styrene-alkyl acrylate-hydroxyethyl(meth)acrylate copolymer.
, _______________________________________________________________________________ __________________________________ Latex Latex Latex Latex Dextrin PVA Ply bond Dry Wet Adhesion TESA
Plex- trial trial trial EMDEX Mowiol strength breaking breaking test tol product product 2 product 3 B1102 4-98 strength strength UF glue 2h X4340 1 3% 6% HEMA 6% HEMA
HEMA
MD/CD MD/CD
Tg= Tg= 40 C Tg= 39 C
28 C Tg= 36 C
, _______________________________________________________________________________ __________________________________ %/wt %/wt %/wt %/wt %/wt J/m2 N/mm- N/mm2 Score Score (bone (bone (bone (bone (bone dry) dry) dry) dry) dry) o , N.) m B-1 45 55 0 1620 74/42 30/25 1 2 g 0.
76/41 38/29 1 1 w N.) N.) 75 / 41 31 / 27 1 2 r r io 76 / 43 39 / 30 2,5 1 0 , _______________________________________________________________________________ __________________________________ .
69/41 23/24 1 2,5 Table 1 above shows the composition of impregnating resin solution and test results.
Claims (17)
1. A prepreg comprising a decorative base paper partially impregnated with an impregnating resin solution, wherein the impregnating resin solution contains at least one styrene-alkylacrylate-hydroxyethyl-(meth)acrylate copolymer and at least one water-soluble polymer, selected from starch or a starch derivative, wherein alkylacrylate is selected from the group consisting of methylacrylate, ethylacrylate, propylacrylate, or butylacrylate or mixtures thereof; and wherein the styrene-alkylacrylate-hydroxyethyl(meth)-acrylate copolymer contains a fraction from 0.5 to 20% by weight hydroxyethylmethacrylate relative to the weight of the acrylate component.
2. The prepreg of claim 1, wherein the fraction of hydroxyethylmethacrylate is 1 to 10%
by weight relative to the mass of the acrylate component.
by weight relative to the mass of the acrylate component.
3. The prepreg of claim 1, wherein the styrene-alkylacrylate-hydroxyethyl-(meth)acrylate copolymer is a styrene-ethylacrylate- hydroxyethylmethacrylate copolymer or a styrene-butylacrylate-hydroxyethylmethacrylate copolymer.
4. The prepreg of claim 1, wherein the copolymer has a glass transition temperature from 35 to 50° C.
5. The prepreg of claim 1, wherein the water-soluble polymer is starch dextrin.
6. The prepreg of claim I , wherein the ratio of water-soluble polymer to copolymer is from 30:70 to 80:20 relative to the mass of impregnating resin (bone dry).
7. The prepreg of claim 1, wherein the impregnating resin solution contains 1 to 30% by weight of a pigment and/or filler relative to the mass of the binding agent (bone dry).
8. The prepreg of claim 7, wherein the pigment is selected from the group consisting of:
titanium dioxide, kaolin, bentonite, calcium carbonate or any combination thereof.
titanium dioxide, kaolin, bentonite, calcium carbonate or any combination thereof.
9. The prepreg of claim 1, wherein the impregnating resin solution has a solid content of 9 to 40% by weight.
10. The prepreg of claim 1, wherein the mass of the impregnating resin in the prepreg, calculated as a dry substance, is 10 to 35% of the grammage of the decorative base paper.
11. The prepreg of claim 1, wherein additional impregnating resin solution is thoroughly applied to the prepreg in order to make a decorative paper or decorative coating material.
12. The prepreg of claim 1, comprising a decorative base paper partially impregnated with an impregnating resin solution, wherein, the impregnating resin solution contains at least one styrene-alkylacrylate-hydroxyethyl-(meth)acrylate copolymer and at least one water-soluble polymer, selected from starch or a starch derivative, wherein alkylacrylate is selected from the group consisting of: methylacrylate, ethylacrylate, propylacrylate, or butylacrylate; the styrene-alkylacrylate-hydroxyethyl(meth)-acrylate copolymer contains a fraction from 0.5 to 20% by weight hydroxyethylmethacrylate relative to the weight of the acrylate component;
the copolymer has a glass transition temperature from 35 to 50° C.; the ratio of water-soluble polymer to copolymer is from 30:70 to 80:20 relative to the mass of impregnating resin; the impregnating resin solution contains 1 to 30% by weight of a pigment and/or filler relative to the mass of the binding agent; and the impregnating resin solution has a solid content of 9 to 40% by weight.
the copolymer has a glass transition temperature from 35 to 50° C.; the ratio of water-soluble polymer to copolymer is from 30:70 to 80:20 relative to the mass of impregnating resin; the impregnating resin solution contains 1 to 30% by weight of a pigment and/or filler relative to the mass of the binding agent; and the impregnating resin solution has a solid content of 9 to 40% by weight.
13. The prepreg of claim 12, wherein, said styrene-alkylacrylate-hydroxyethyl-(meth)acrylate copolymer is a styreneethylacrylate- hydroxyethylmethacrylate copolymer or a styrene-butylacrylate-hydroxyethylmethacrylate copolymer; said styrene-alkylacrylate-hydroxyethyl(meth)-acrylate copolymer contains a fraction from 1 to 10% by weight hydroxyethylmethacrylate relative to the weight of the acrylate component; and said water-soluble polymer is selected from the group consisting of: a starch, starch derivative, starch dextrin, or any combination of thereof.
14. The prepreg of claim 13, wherein, said styrene-alkylacrylate-hydroxyethyl(meth)-acrylate copolymer contains a fraction from 3 to 8% by weight hydroxyethylmethacrylate relative to the weight of the acrylate component; said pigment is selected from the group consisting of: titanium dioxide, kaolin, bentonite, calcium carbonate or any combination thereof and said mass of the impregnating resin in the prepreg, calculated as a dry substance, is 10 to 35% of the grammage of the decorative base paper.
15. A decorative paper or decorative coating material comprising a decorative base paper thoroughly impregnated with an impregnating resin solution, wherein the impregnating resin solution contains at least one styrene-alkylacrylate-hydroxyethyl -(meth)acrylate copolymer and at least one water-soluble polymer, wherein alkylacrylate is selected from the group consisting of: methylacrylate, ethylacrylate, propylacrylate, or butylacrylate or mixtures thereof; and wherein the styrene-alkylacrylate -hydroxyethyl(meth)-acrylate copolymer contains a fraction from 0.5 to 20% by weight hydroxyethylmethacrylate relative to the weight of the acrylate component.
16. A process for manufacturing a prepreg, the process comprising partially impregnating a decorative base paper with an impregnating resin solution, wherein the impregnating resin solution contains at least one styrene-alkylacrylate-hydroxyethyl-(meth)acrylate copolymer and at least one water-soluble polymer, selected from starch or a starch derivative, wherein alkylacrylate is selected from the group consisting of: methylacrylate, ethylacrylate, propylacrylate, or butylacrylate or mixtures thereof; and wherein the styrene-alkylacrylate-hydroxyethyl(meth)-acrylate copolymer contains a fraction from 0.5 to 20% by weight hydroxyethylmethacrylate relative to the weight of the acrylate component.
17. A process for manufacturing a decorative paper or decorative coating material, the process comprising thoroughly impregnating a decorative base paper with an impregnating resin solution, wherein the impregnating resin solution contains at least one styrene-alkylacrylate-hydroxyethyl-(meth)acrylate copolymer and at least one water-soluble polymer, selected from starch or a starch derivative, wherein alkylacrylate is selected from the group consisting of: methylacrylate, ethylacrylate, propylacrylate, or butylacrylate or mixtures thereof: and wherein the styrene-alkylacrylate-hydroxyethyl(meth)-acrylate copolymer contains a fraction from 0.5 to 20% by weight hydroxyethylmethacrylate relative to the weight of the acrylate component.
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DE102011105676.2A DE102011105676B4 (en) | 2011-06-22 | 2011-06-22 | Prepreg and decorative paper or decorative coating material therefrom |
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EP (1) | EP2537682B1 (en) |
JP (1) | JP5826717B2 (en) |
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CN (1) | CN102837554B (en) |
BR (1) | BR102012015673B1 (en) |
CA (1) | CA2780543C (en) |
CL (1) | CL2012001708A1 (en) |
DE (1) | DE102011105676B4 (en) |
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EP2780507B1 (en) * | 2011-11-18 | 2017-01-04 | Roquette Frères | Coating slips based on partially soluble dextrins of high molecular weight |
EP3023261B1 (en) | 2014-11-20 | 2017-03-15 | Flooring Technologies Ltd. | Method for finishing a wooden material panel |
EP3253920B1 (en) * | 2015-02-04 | 2018-12-12 | Ahlstrom-Munksjö Dettingen GmbH | Composition and method for producing pre-impregnated decorative base paper comprising biopolymer nanoparticles |
EP3754109B1 (en) | 2019-06-18 | 2022-09-28 | Schoeller Technocell GmbH & Co. KG | Pre-impregnate with improved flatness |
JP2022048546A (en) * | 2020-09-15 | 2022-03-28 | セイコーエプソン株式会社 | Composite, molding, and production method of molding |
DE102022115834A1 (en) * | 2022-06-24 | 2024-01-04 | Oskar Nolte Gmbh | Aqueous top coat composition for decorative finish films |
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US20120325418A1 (en) | 2012-12-27 |
JP5826717B2 (en) | 2015-12-02 |
BR102012015673B1 (en) | 2020-03-03 |
US8916027B2 (en) | 2014-12-23 |
BR102012015673A2 (en) | 2013-07-09 |
DE102011105676A1 (en) | 2012-12-27 |
KR101939312B1 (en) | 2019-04-11 |
RU2012125957A (en) | 2013-12-27 |
CL2012001708A1 (en) | 2013-01-25 |
PL2537682T3 (en) | 2016-06-30 |
JP2013028802A (en) | 2013-02-07 |
CA2780543A1 (en) | 2012-12-22 |
UA115300C2 (en) | 2017-10-25 |
CN102837554B (en) | 2017-03-01 |
DE102011105676B4 (en) | 2018-05-09 |
RU2607582C2 (en) | 2017-01-10 |
CN102837554A (en) | 2012-12-26 |
KR20130000351A (en) | 2013-01-02 |
EP2537682B1 (en) | 2016-01-06 |
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